CN101654318B - Excrement centralized processing method - Google Patents
Excrement centralized processing method Download PDFInfo
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- CN101654318B CN101654318B CN2009100924437A CN200910092443A CN101654318B CN 101654318 B CN101654318 B CN 101654318B CN 2009100924437 A CN2009100924437 A CN 2009100924437A CN 200910092443 A CN200910092443 A CN 200910092443A CN 101654318 B CN101654318 B CN 101654318B
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Abstract
The invention relates to an excrement centralized processing method, comprising the steps of solid-liquid separation, flocculation water removing, aerobic compost treatment, anaerobic sewage treatment, facultative anaerobic sewage treatment, aerobic sewage treatment, membrane anaerobic reacting sewage treatment and odor treatment. Treated with the processing method of the invention, the urban night soil is 100% decontaminated, is 99.7% minimized and the excrement sludge is completely changed into resource.
Description
Technical field
The present invention relates to a kind of urban night soil treatment process, particularly a kind of urban night soil is innoxious, minimizing, recycling treatment process.
Background technology
Along with quickening of urbanization process, ight soil becomes each metropolitan puzzlement day by day.Only just there are more than 1,650 ten thousand people Beijing by statistical result showed in 2006, calculate to discharge 500g ight soil for each person every day, just there are every day 825 kilograms ight soil to produce, nitrogenous 18.6 grams, phosphorus 1.74 restrain in the ight soil of Pai Chuing for each person every day, can pollute 10 tons of water bodys, 825 kilograms ight soil just can pollute 8,250,000 tons of water bodys.Can not allow the fecal pollution water source, bring huge pressure can for again the municipal wastewater treatment system, cause water outlet not up to standard but ight soil directly enters city planting ductwork, even the total system paralysis.It is untimely that ight soil is handled, and can scatter by foul smell, and mosquito, fly, maggot multiply, become spread germs, the hotbed of virus.So it is imperative that innoxious, the minimizing of ight soil is handled, but ight soil itself contains abundant biochemical substances and nitrogen, phosphatic manure material, is the best outlet of ight soil to its recycling.
Existing urban night soil treatment system is that solid landfill, liquid directly enter city planting ductwork through after the solid-liquid separation mostly, brings very big pressure not only for garbage loading embeading factory and municipal wastewater treatment system, and has wasted the resource material in the ight soil.
Summary of the invention
The objective of the invention is in order to solve the difficult problem that existing urban night soil is handled.Provide that a kind of urban night soil is innoxious, the treatment process of minimizing and resource utilization.This method is admitted the ight soil of the public lavatory septic tank of canned fortune dung-cart transportation, and through handling, Beijing's pollution discharge standard is satisfied in draining, and can produce biogas and two kinds of energy of fertilizer.
In order to finish the application's goal of the invention, the present invention by the following technical solutions:
The method that a kind of ight soil of the present invention focuses on, it may further comprise the steps:
(1) solid-liquid separation; Ight soil enters solid-liquid separation system by the closed feces-discharging mouth, with particle diameter in the ight soil is that solids more than the 10mm is removed, the water ratio of isolated solids is between 45%～70%, solids by using sealing isolation is slagged tap and the airtight landfill disposal of transporting, solid content is lower than 5% in the sewage after treatment, sewage is sent into carried out homogeneous, all amount and temporary transient storages in first equalizing tank;
(2) flocculation dewatering: the sewage in first equalizing tank is entered the flocculation reaction jar via lift pump, at weight percent is the flocculation agent effect of sewage 0.005%-0.015%, to generate the copropel flco less than solid substance that equals 10mm and colloid in the sewage, the copropel flco enters and carries out extrusion dehydration in the screw extrusion dewatering unit, the sewage that obtains after the dehydration enters second equalizing tank, and the copropel that obtains after the dehydration enters aerobic compost by worm conveyor and handles;
(3) aerobic compost: the copropel that step (2) obtains is sent into the compost workshop by worm conveyor, this copropel water ratio is 65-70%, particle diameter is smaller or equal to 10mm, the external auxiliary material and the copropel that account for copropel weight 25-35% are sent into composting in the compost groove after stirrer for mixing is even, wherein external auxiliary material be water ratio less than 35% particle diameter less than the vegetalitas stalk of 4mm or/and leaf or/and sawdust, this windrow water ratio is 55-65%, in temperature is under 55-65 ℃, adopt aerobic aeration or/and the mode of aerobic negative inspiratory pressure is banked up more than 5 days to above-mentioned windrow, every day with the overturning of slurry formula stack turner once;
(4) anaerobic treatment of sewage; The sewage that step (2) obtains is delivered to upflow anaerobic sludge blanket reactor from second equalizing tank through lift pump, anaerobic sludge is housed in the upflow anaerobic sludge blanket reactor, the content of anaerobic sludge in sewage is at least 10,000 mg/litre, and the volumetric loading of chemical oxygen demand is 3-6kgCOD/m
3.d, sewage stopped in upflow anaerobic sludge blanket reactor 1-3 days, organism in the sewage is degraded, and be simple, stable relatively compound with the organic compound Degradation and Transformation of complexity, discharge biogas simultaneously, biogas feeds gas-storing bag or gas storage holder stores, and anaerobic sludge increases the remaining mud that produces and turns back in first equalizing tank of step (1);
(5) the double oxygen of sewage is handled; Sewage after step (4) processing is sent in the oxygen compatibility pool, hold concurrently oxygen mud and autotrophic denitrification granular filler are housed in the oxygen compatibility pool, the content of oxygen mud in sewage of holding concurrently is at least 10,000 mg/litre, the autotrophic denitrification granular filler is to be that 1: 10 to 10: 1 sulphur and lime carbonate sintering forms by ratio, the autotrophic denitrification granular filler accounts for the 5%-15% of oxygen compatibility pool cumulative volume, sewage sewage in oxygen compatibility pool stopped 1-2 hour, removed the nitrate more than 90% in the sewage, the oxygen mud of holding concurrently increases the excess sludge that produces and turns back in first equalizing tank of step (1);
(6) aerobic treatment of sewage: the sewage after step (5) processing is sent in the Aerobic Pond, aerobic sludge is housed in the Aerobic Pond, the content of aerobic sludge in sewage is at least 10,000 mg/litre, the ratio of oxygen is more than 2 mg/litre in Aerobic Pond, sewage stopped in Aerobic Pond 5-10 hour, make the ammonia nitrogen of 80-90% in the sewage be degraded and be converted into nitric nitrogen and the organism more than 95% of degrading that aerobic sludge increases the excess sludge that produces and turns back in first equalizing tank of step (1);
(7) membrane biological reaction of sewage is handled: the sewage after step (6) is handled is sent into the membrane biological reaction pond, in the membrane biological reaction pond, membrane bioreactor is housed, sewage enters from the micropore on film surface, the water of discharging from center membrane is discharged into the municipal wastewater pipeline, the concentration of the oxygen in water that wherein is discharged is more than 2 mg/litre, and the 1/5-1/2 that is filtered out sewage by membrane bioreactor does not return in the oxygen compatibility pool of step (5) and handles;
(8) stink is administered, and flocculation reaction jar neutralization procedure (3) aerobic compost in the solid-liquid separation system and first equalizing tank in the step (1), in the step (2) is handled the foul smell that discharges collect, and concentrates through the biological deodorizing method and administers;
The method that ight soil of the present invention focuses on, wherein: described step (4) is in (6), in upflow anaerobic sludge blanket reactor, oxygen compatibility pool and Aerobic Pond in above-mentioned steps, when the mud total content surpasses 1.5 ten thousand mg/litre, from above-mentioned upflow anaerobic sludge blanket reactor, oxygen compatibility pool and Aerobic Pond, discharge mud respectively, till sludge content reaches 10,000 mg/litre to first equalizing tank;
The method that ight soil of the present invention focuses on, wherein: the flocculation agent in the described step (2) is a polyacrylamide;
The method that ight soil of the present invention focuses on, wherein: described fecal sewage is 15-25% with potassium bichromate as the chemical oxygen demand concentration clearance that oxygenant determines sewage after step (1) is handled;
The method that ight soil of the present invention focuses on, wherein: the solid content after the flocculation treatment in the described step (2) in the sewage determines the chemical oxygen demand clearance of sewage greater than 50% with potassium bichromate as oxygenant less than 0.5%;
The method that ight soil of the present invention focuses on, wherein: aerobic aeration is in the compost bottom aeration tube and aerator to be installed in the described step (3), and air is blasted from the compost bottom surface, and the foul smell that compost discharges is concentrated through the stink governing system and administered;
The method that ight soil of the present invention focuses on, wherein: aerobic negative inspiratory pressure is in the compost bottom extraction pipe and vacuum fan to be installed in the described step (3), air is entered from the compost surface, by the extraction pipe and the vacuum fan of bottom, the stink governing system of the foul smell that compost discharges through linking to each other with vacuum fan concentrated and administered;
The method that ight soil of the present invention focuses on, wherein: sewage is handled through the oxygen of holding concurrently of sending into behind the triphase separator in the described step (4), biogas through behind the triphase separator send into gas-storing bag or gas storage holder is temporary.
Urban night soil of the present invention is innoxious, the advantage of minimizing, process for reclaiming:
1. ight soil at first passes through solid-liquid separation, has not only avoided the large particulate matter blocking pipeline but also can remove chemical oxygen demand about 20%;
The flocculation dewatering step can remove more than 50% chemical oxygen demand, reduce the load of subsequent wastewater treatment step;
3. the aerobic compost step has realized the innoxious and resource utilization of dehydration copropel;
4. the aerobic compost step can be selected positive aeration or aerobic negative inspiratory pressure dual mode according to conditions such as seasons;
5. oxygen compatibility pool has added the autotrophic denitrification granular filler, can guarantee that the nitrogen content of water outlet is qualified;
6. the high concentration sludge of membrane cisterna can guarantee that pollutents such as phosphorus, organism are qualified;
7. the patented technology of our company is adopted in stink control, makes the gas of discharging reach GB14554-1993 " odorant pollutant emission standard " requirement;
8. in sum, the present invention realized that urban night soil is innoxious, the processing intent of minimizing, resource utilization.
Description of drawings
The process frame chart of the method that Fig. 1 focuses on for ight soil of the present invention.
Embodiment
As shown in Figure 1, the method that focuses on of ight soil of the present invention adopts following steps:
(1) solid-liquid separation
Fecal sewage enters the excrement solid-liquid separation system by feces-discharging mouth, and the processing power of solid-liquid separation system is 1.5-2.5m
3/ min impacts ability to accept 3m
3/ min.With particle diameter in the ight soil foreign material is that solids more than the 10mm is removed, and solid content is lower than 5% in the filtrate after treatment, and isolated solids water ratio is between 45%～70%.Isolated solid slag adopts airtight transporting to slag tap, and airtightly is transported to refuse landfill and handles.Filtered liquid enters first equalizing tank, and first equalizing tank mainly plays the effect that homogeneous is all measured and temporarily store in this treatment system, handles in order to entering next processing unit.Final solids discharge port height is not less than 1.4m; During working order, be the fully-closed form, do not have obvious foul gas leakage point; The contact element of all and ight soil all adopts stainless steel AISI 304 to make, and fecal sewage is 15-25% with potassium bichromate as the chemical oxygen demand concentration clearance that oxygenant determines sewage after solid-liquid separation is handled.
(2) flocculation dewatering
The sewage of first equalizing tank is squeezed into the flocculation reaction jar via lift pump, flocculation reaction jar processing power 12m
3/ h, liquid manure enter this section interpolation flocculation agent, and the liquid manure that adds flocculation agent fully flocculates and dewaters at this section warp.The flocculation agent addition is the 0.005%-0.015% of sewage gross weight, and flocculation agent is a polyacrylamide.Solid content is less than 0.5% in the water outlet after the flocculation.The chemical oxygen demand clearance is greater than 50%.Sewage behind the flocculation dewatering enters second equalizing tank; And the copropel that produces in the flocculation process enters the aerobic compost system.During working order, be the fully-closed form, do not have obvious foul gas leakage point; The contact element of all and sewage all adopts stainless steel AISI 304 to make.
(3) aerobic compost
Copropel after the flocculation enters the compost workshop by Shaftless screw conveyor, mixes the fertile processing of laggard windrow with the outer supplied materials that accounts for copropel weight 25-35%.The copropel water ratio is 65-70%, compost ability 15-20 every day ton.External auxiliary material be water ratio less than 35% particle diameter less than the vegetalitas stalk of 4mm or/and leaf or/and sawdust.The windrow water ratio is 55-65%, is under 55-65 ℃ in temperature, adopts aerobic aeration or/and the mode of aerobic negative inspiratory pressure is banked up more than 5 days to above-mentioned windrow, and every day with the overturning of slurry formula stack turner once; The aerobic negative inspiratory pressure of compost is in the compost bottom extraction pipe and vacuum fan to be installed, air is entered from the compost surface, by the extraction pipe and the vacuum fan of bottom, foul smell such as ammonia, stink damp etc. that compost discharges are collected concentrated improvement from the stink governing system that links to each other with vacuum fan.Aerobic aeration is in the compost bottom aeration tube and aerator to be installed, and air is blasted from the compost bottom surface, and the foul smell that compost discharges links to each other with the stink governing system to concentrate and administers.Aerobic compost can adopt aerobic aeration or aerobic negative inspiratory pressure, as adopting aerobic aeration winter, adopts aerobic negative inspiratory pressure other seasons.
(4) anaerobic treatment of sewage;
The sewage that step (2) obtains is delivered to upflow anaerobic sludge blanket reactor from second equalizing tank through lift pump, anaerobic sludge is housed in the upflow anaerobic sludge blanket reactor, the content of anaerobic sludge in sewage is at least 10,000 mg/litre, and the volumetric loading of chemical oxygen demand is 3-6kgCOD/m
3.d, sewage stopped in upflow anaerobic sludge blanket reactor 1-3 days, organism in the sewage is degraded, with the organic compound Degradation and Transformation of complexity is simple, stable relatively compound, discharge biogas simultaneously, biogas feeds gas-storing bag or gas storage holder stores, biogas uses of can generating electricity or live, and the excess sludge that anaerobic sludge increases generation turns back in first equalizing tank of step (1);
(5) the double oxygen of sewage is handled;
Sewage after step (4) processing is sent in the oxygen compatibility pool, hold concurrently oxygen mud and autotrophic denitrification granular filler are housed in the oxygen compatibility pool, the content of oxygen mud in sewage of holding concurrently is at least 10,000 mg/litre, the autotrophic denitrification granular filler is to be that 1: 10 to 10: 1 sulphur and lime carbonate sintering under 450-750 ℃ of high temperature forms by ratio, the autotrophic denitrification granular filler accounts for the 5%-15% of oxygen compatibility pool volume, sewage sewage in oxygen compatibility pool stopped 1-2 hour, removed the nitrate more than 90% in the sewage, the oxygen mud of holding concurrently increases the excess sludge that produces and turns back in first equalizing tank of step (1);
(6) aerobic treatment of sewage:
Sewage after step (5) processing is sent in the Aerobic Pond, aerobic activated sludge is housed in the Aerobic Pond, the content of aerobic sludge in sewage is at least 10,000 mg/litre, the ratio of oxygen is more than 2 mg/litre in Aerobic Pond, sewage stopped in Aerobic Pond 5-10 hour, make the ammonia nitrogen of 80-90% in the sewage be degraded and be converted into nitric nitrogen and the organism more than 95% of degrading that aerobic sludge increases the excess sludge that produces and turns back in first equalizing tank of step (1);
(7) membrane biological reaction of sewage is handled:
For preventing fiber fines shape materials such as solid matter bigger in the sewage, fiber fines and hair, film is caused damage, the grid of 1mm is adopted in design before the membrane biological reaction groove, and sewage enters the biomembrane reaction pond behind grid filtration, and the grid slag of grid regularly cleans automatically.
Sewage after step (6) processing is sent into the membrane biological reaction pond, in the membrane biological reaction pond, membrane bioreactor is housed, sewage enters from the micropore on film surface, the water of discharging from center membrane is discharged into the municipal wastewater pipeline, the concentration of the oxygen in water that wherein is discharged is more than 2 mg/litre, and the 1/5-1/2 that is filtered out sewage by membrane bioreactor does not return in the oxygen compatibility pool of step (5) and handles;
Membrane biological reaction is handled except the active dirt that can keep high density, filteration is the another outstanding feature of film, the suspended substance that gets water outlet after membrane biological reaction filters is very low, and chemical oxygen demand, biological oxygen demand (BOD), oil, fat etc. are held back removal to a certain extent in the water, and water outlet can be satisfied and reaches the limit value requirement that " Beijing's pollution discharge standard " enters sewer pipeline.
(8) stink is administered, and the foul smell that flocculation reaction jar neutralization procedure (3) compost treatment in the solid-liquid separation system and first equalizing tank in the step (1), in the step (2) discharges is collected, and removes foul smell through the biological deodorizing method.My house journal's technology is adopted in odor treatment, and the patent No. is ZL2008 2 0004952.0.This patent adopts biologic deodorization method, with in the treatment station each let out smelly point by the ventilation system centralized collection in the district of station in the deodorizing tower of bacteria bed formula, the adsorption of the filtering layer of various different biologic packing materials in the process tower, removed in the foul smell the smelly compound that causes more than 99%, the tail gas of being discharged by the biological deodorizing tower can directly enter the chimney high altitude discharge.
In step (4) in (6), in upflow anaerobic sludge blanket reactor, oxygen compatibility pool and Aerobic Pond in above-mentioned steps, when the mud total content surpasses 1.5 ten thousand mg/litre, from above-mentioned upflow anaerobic sludge blanket reactor, oxygen compatibility pool and Aerobic Pond and membrane biological reaction pond, discharge mud respectively, reach 10,000 mg/litre up to sludge content to first equalizing tank.
Above embodiment is an explanation of the invention, is not that institute of the present invention restricted portion is referring to claim to the qualification of invention, and under the situation of spirit of the present invention, the present invention can do any type of modification.
Claims (8)
1. method that ight soil focuses on, it may further comprise the steps:
(1) solid-liquid separation; Ight soil enters solid-liquid separation system by the closed feces-discharging mouth, with particle diameter in the ight soil is that solids more than the 10mm is removed, the water ratio of isolated solids is between 45%～70%, solids by using sealing isolation is slagged tap and the airtight landfill disposal of transporting, solid content is lower than 5% in the sewage after treatment, sewage is sent into carried out homogeneous, all amount and temporary transient storages in first equalizing tank;
(2) flocculation dewatering: the sewage in first equalizing tank is entered the flocculation reaction jar via lift pump, at weight percent is the flocculation agent effect of sewage 0.005%-0.015%, to generate the copropel flco less than solid substance that equals 10mm and colloid in the sewage, the copropel flco enters and carries out extrusion dehydration in the screw extrusion dewatering unit, the sewage that obtains after the dehydration enters second equalizing tank, and the copropel that obtains after the dehydration enters aerobic compost by worm conveyor and handles;
(3) aerobic compost: the copropel that step (2) obtains is sent into the compost workshop by worm conveyor, this copropel water ratio is 65-70%, particle diameter is smaller or equal to 10mm, the external auxiliary material and the copropel that account for copropel weight 25-35% are sent into composting in the compost groove after stirrer for mixing is even, wherein external auxiliary material be water ratio less than 35% particle diameter less than the vegetalitas stalk of 4mm or/and leaf or/and sawdust, this windrow water ratio is 55-65%, in temperature is under 55-65 ℃, adopt aerobic aeration or/and the mode of aerobic negative inspiratory pressure is banked up more than 5 days to above-mentioned windrow, every day with the overturning of slurry formula stack turner once;
(4) anaerobic treatment of sewage; The sewage that step (2) obtains is delivered to upflow anaerobic sludge blanket reactor from second equalizing tank through lift pump, anaerobic sludge is housed in the upflow anaerobic sludge blanket reactor, the content of anaerobic sludge in sewage is at least 10,000 mg/litre, and the volumetric loading of chemical oxygen demand is 3-6kgCOD/m
3D, sewage stopped in upflow anaerobic sludge blanket reactor 1-3 days, organism in the sewage is degraded, and be simple, stable relatively compound with the organic compound Degradation and Transformation of complexity, discharge biogas simultaneously, biogas feeds gas-storing bag or gas storage holder stores, and anaerobic sludge increases the remaining mud that produces and turns back in first equalizing tank of step (1);
(5) the double oxygen of sewage is handled; Sewage after step (4) processing is sent in the oxygen compatibility pool, hold concurrently oxygen mud and autotrophic denitrification granular filler are housed in the oxygen compatibility pool, the content of oxygen mud in sewage of holding concurrently is at least 10,000 mg/litre, the autotrophic denitrification granular filler is to be that 1: 10 to 10: 1 sulphur and lime carbonate sintering forms by ratio, the autotrophic denitrification granular filler accounts for the 5%-15% of oxygen compatibility pool cumulative volume, sewage sewage in oxygen compatibility pool stopped 1-2 hour, removed the nitrate more than 90% in the sewage, the oxygen mud of holding concurrently increases the excess sludge that produces and turns back in first equalizing tank of step (1);
(6) aerobic treatment of sewage: the sewage after step (5) processing is sent in the Aerobic Pond, aerobic sludge is housed in the Aerobic Pond, the content of aerobic sludge in sewage is at least 10,000 mg/litre, the ratio of oxygen is more than 2 mg/litre in Aerobic Pond, sewage stopped in Aerobic Pond 5-10 hour, make the ammonia nitrogen of 80-90% in the sewage be degraded and be converted into nitric nitrogen and the organism more than 95% of degrading that aerobic sludge increases the excess sludge that produces and turns back in first equalizing tank of step (1);
(7) membrane biological reaction of sewage is handled: the sewage after step (6) is handled is sent into the membrane biological reaction pond, in the membrane biological reaction pond, membrane bioreactor is housed, sewage enters from the micropore on film surface, the water of discharging from center membrane is discharged into the municipal wastewater pipeline, the concentration of the oxygen in water that wherein is discharged is more than 2 mg/litre, and the 1/5-1/2 that is filtered out sewage by membrane bioreactor does not return in the oxygen compatibility pool of step (5) and handles;
(8) stink is administered, and flocculation reaction jar neutralization procedure (3) aerobic compost in the solid-liquid separation system and first equalizing tank in the step (1), in the step (2) is handled the foul smell that discharges collect, and concentrates through the biological deodorizing method and administers.
2. the method that ight soil as claimed in claim 1 focuses on, it is characterized in that: described step (4) is in (6), in upflow anaerobic sludge blanket reactor, oxygen compatibility pool and Aerobic Pond in above-mentioned steps, when the mud total content surpasses 1.5 ten thousand mg/litre, from above-mentioned upflow anaerobic sludge blanket reactor, oxygen compatibility pool and Aerobic Pond, discharge mud respectively, till sludge content reaches 10,000 mg/litre to first equalizing tank.
3. the method that ight soil as claimed in claim 2 focuses on is characterized in that: the flocculation agent in the described step (2) is a polyacrylamide.
4. the method that ight soil as claimed in claim 3 focuses on is characterized in that: described fecal sewage is 15-25% with potassium bichromate as the chemical oxygen demand concentration clearance that oxygenant determines sewage after step (1) is handled.
5. the method that ight soil as claimed in claim 4 focuses on is characterized in that: the solid content after the flocculation treatment in the described step (2) in the sewage determines the chemical oxygen demand clearance of sewage greater than 50% with potassium bichromate as oxygenant less than 0.5%.
6. the method that ight soil as claimed in claim 5 focuses on, it is characterized in that: aerobic aeration is in the compost bottom aeration tube and aerator to be installed in the described step (3), air is blasted from the compost bottom surface, and the foul smell that compost discharges is concentrated through the stink governing system and is administered.
7. the method that ight soil as claimed in claim 5 focuses on, it is characterized in that: aerobic negative inspiratory pressure is in the compost bottom extraction pipe and vacuum fan to be installed in the described step (3), air is entered from the compost surface, by the extraction pipe and the vacuum fan of bottom, the stink governing system of the foul smell that compost discharges through linking to each other with vacuum fan concentrated and administered.
8. the method that focuses on as claim 6 or 7 described ight soil, it is characterized in that: sewage is handled through sending into the oxygen of holding concurrently behind the triphase separator in the described step (4), and biogas is sent into gas-storing bag or gas storage holder through behind the triphase separator.
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| CN2009100924437A CN101654318B (en) | 2009-09-08 | 2009-09-08 | Excrement centralized processing method |
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| CN2009100924437A CN101654318B (en) | 2009-09-08 | 2009-09-08 | Excrement centralized processing method |
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